EP0436787B1 - Fliessbettapparatur zum Herstellen und/oder Weiterbehandeln schüttfähigen Gutes - Google Patents

Fliessbettapparatur zum Herstellen und/oder Weiterbehandeln schüttfähigen Gutes Download PDF

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Publication number
EP0436787B1
EP0436787B1 EP90120199A EP90120199A EP0436787B1 EP 0436787 B1 EP0436787 B1 EP 0436787B1 EP 90120199 A EP90120199 A EP 90120199A EP 90120199 A EP90120199 A EP 90120199A EP 0436787 B1 EP0436787 B1 EP 0436787B1
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EP
European Patent Office
Prior art keywords
fluidized bed
lance
bed apparatus
gas
trough
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP90120199A
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German (de)
English (en)
French (fr)
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EP0436787A3 (en
EP0436787A2 (de
Inventor
Herbert Hüttlin
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Individual
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Individual
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Filing date
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Publication of EP0436787A2 publication Critical patent/EP0436787A2/de
Publication of EP0436787A3 publication Critical patent/EP0436787A3/de
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Publication of EP0436787B1 publication Critical patent/EP0436787B1/de
Anticipated expiration legal-status Critical
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/386—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/16—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas

Definitions

  • the process chamber is the circular interior of a container which is rotationally symmetrical with respect to a vertical axis.
  • the process chamber contains a ring of guide vanes which, viewed in the direction of the container axis, overlap one another and impart a swirl to the upward gas flow.
  • lances each having a plurality of material discharge nozzles arranged in the flow direction of the gas. These nozzles can be used to spray large amounts of powdery and / or liquid substance per unit of time into a fluidized bed formed above the guide vanes.
  • Granular material which has been produced and / or further processed in this known fluid bed apparatus is distinguished by a particularly high degree of homogeneity. For example, a narrow range of grain sizes can be achieved in the manufacture of build-up granules, and coating processes result in coating coatings of particularly uniform thickness.
  • pellets with varnish coatings of different composition or thickness are occasionally required so that certain active substances are released in specific areas of the human gastrointestinal tract.
  • such different pellets had to be produced in batches in the known apparatus, whereby longer interruptions in operation were unavoidable for converting the apparatus to different operating conditions.
  • the batch size can only be varied within relatively narrow limits, so that production with such a fluid bed apparatus cannot readily be adapted to different operational requirements.
  • the invention is therefore based on the object of designing a fluidized bed apparatus for producing and / or further treating pourable goods from solid moldings in such a way that that it can be easily adapted to different requirements of the type described.
  • a trough according to the invention of a given total length can form a single straight-line treatment section in a correspondingly elongated housing or can be divided into several sections which can be arranged next to one another in a space-saving manner in a common housing.
  • the same or different treatment steps can be carried out simultaneously in more or less long sections of the trough and sections that are not required can be shut down, for example by inserting partitions.
  • the fluidized bed apparatus shown in FIGS. 1 to 4 has a housing 10 which forms an oblong cuboid in the horizontal direction and has heat-insulated walls.
  • Six process chambers 12 are formed within the housing 10, each having a common base 14, two gas inlets 16 arranged in the base as well as gas outlets 18, five of which are each assigned to two adjacent process chambers 12.
  • the gas inlets 16 connect the process chambers 12 to a common supply air chamber 20 which is arranged under the base 14 and which is to be supplied with dehumidified warm air or another process gas via connections 22.
  • the gas outlets 18 open into exhaust air chambers 24, which are arranged on the long sides of the housing 10 and extend to below the base 14, where they pass through connections 26 can be connected to the suction side of a conventional blower.
  • each of the process chambers 12 is closed during operation with a cover 28, which is made of glass, for example, and can be swung up for cleaning purposes.
  • a gas-permeable conveyor belt 30 extends through the entire housing 10 in the longitudinal direction thereof, for example a known link belt made of metal or plastic wire helices.
  • the conveyor belt 30 can be pulled off a decoiler 32 and can be wound up on a decoiler 34 after use. Instead of these two reels 32 and 34, deflection rollers can be provided, which are wrapped around by an endless conveyor belt.
  • the end faces at which the conveyor belt 30 enters and exits the housing 10 are normally closed by a flap 36.
  • a film 38 is placed on a section of the conveyor belt 30 that is somewhat longer than the housing 10, which film is then brought into the housing 10 by moving the conveyor belt 30, with one in the process chambers 12 Loaded manufactured or treated goods and is moved out of the housing 10 together with this by moving the conveyor belt 30 again. As indicated in FIG. 1, the film 38 is pulled upwards so far at the lateral boundaries of the process chambers 12 that contamination of the conveyor belt 30 with the manufactured and / or treated material is prevented.
  • a lance 40 extends horizontally through each process chamber 12 at a distance above the floor 14.
  • Each of the lances 40 has a teardrop-shaped profile which is symmetrical to the central plane A and is rounded at the bottom and pointed at the top.
  • two guide vanes 42 and 44 are arranged parallel to the associated lance 40.
  • each lance 40 The two guide vanes 42 and 44 on one and the other side of each lance 40 are connected to one another by plates 46 which each extend in a vertical longitudinal plane and are fastened on a shaft 48 arranged parallel to the lance 40.
  • the shafts 48 are each connected to a swivel drive 50, for example with a hydraulic or pneumatic rotary vane motor, with which the associated guide vanes 42 and 44 can be pivoted back and forth in an angular range of, for example, 30 °.
  • a half-shell 52 is arranged on each side of each lance 40, also parallel to it.
  • the half shells 52 together with the associated guide vanes 42 and 44 and the lance 40 form a trough 53 which, in the operating position of the guide vanes - sh. in Fig. 2, the second and third process chamber 12 from the right - is almost closed at the bottom, but leaves three gaps B, C and D on both sides of the lance 40, which extend over the entire width of the process chamber 12.
  • Process air in the form of a general gas flow E can flow upward through the column B, C and D around the profile of the lance 40 and a fluidized bed delimited by the trough 53, starting from the associated gas inlets 16 Form F (see FIG. 2 the second chamber from the right and FIG. 3).
  • the guide vanes 42 and 44 can be moved from the operating position into an emptying position by means of the swivel drive 50 - see FIG. in Fig. 2, the first chamber from the right - swivel, in which the material that has collected in the trough 53 after the air flow has stopped can trickle down through the gaps B, C and D onto the film 38.
  • the upper edges of the half-shells 52 in adjacent process chambers 12 leave a space between them which is covered by a concave cover profile 54 seen from below. Between the upper edge of each half-shell 52 and the associated cover profile 54, a gap D 'remains free, through which another part of the general gas flow E flows from top to bottom into the trough 53 in question.
  • the cover profiles 54 are arranged so that the material can flow over them when it exceeds a certain height in one of the troughs 53. Alternatively, adjacent troughs 53 can be separated from one another by an intermediate wall 56.
  • the gas outlets 18 arranged further up are covered by baffle plates 58 in such a way that at most dust-like particles of the material get into the exhaust air chambers 24, where they can be filtered out of the gas stream in the usual way.
  • the apparatus shown in FIGS. 1 to 4 is equipped in all of its process chambers 12 for painting and drying prefabricated moldings P, for example pellets or tablets, which are poured into each individual trough 53 from above, in a fluidized state. 5 to 9, on the other hand, there is the possibility of first extruding particles from doughy mass, then painting them and finally drying them. Since the area of application of the apparatus shown in FIGS. 5 to 9 thus begins at an earlier stage of the manufacturing process, details of this apparatus are described below before further similarities between the two apparatuses are discussed.
  • prefabricated moldings P for example pellets or tablets
  • FIGS. 5 to 7 three elongate process chambers 12, which correspond to those shown in FIGS. 1 to 4, are arranged one behind the other in the housing 12. Of these three process chambers 12, the left one in FIGS. 5 and 6 is used for extrusion, the middle one for painting and the right one for drying.
  • a single lance 40 extends through these three process chambers 12 and is divided into three aligned sections, one for each process chamber 12. All sections of the lance 40 have the outer profile shown in FIG. 7 over their entire length, but only the section in the left process chamber 12 is designed in all details as shown in FIGS. 8 and 9 and described below .
  • the section of the lance 40 in the first process chamber 12 on the left in FIGS. 5 and 6 has a longitudinally extending conveying channel 60 of circular cross-section, which is arranged coaxially with the likewise circular-arc-shaped lower part of the lance profile and extends approximately over the entire length of the first Process chamber 12 extends.
  • a pump 62 for example a commercially available eccentric screw pump, which is driven by an electric motor 64 and presses a doughy mass to be extruded from a container 66 into the delivery channel 60, is laterally connected to the two ends of the delivery channel 60.
  • the section of the lance 40 arranged in the first process chamber 12 contains in its conveying channel 60 a stirrer 68 which can be driven by its own electric motor 69 and ensures that the mass in the conveying channel 60 is constantly stirred and does not solidify.
  • the delivery channel 60 is connected by a longitudinal slot 70 to a distribution channel 72, which also extends in the longitudinal direction of the lance 40, and from which holes are inclined at regular intervals lead up to the surface of the lance 40.
  • the holes each have a shoulder on which they widen outwards and on which there is a sealing ring.
  • a material discharge nozzle 80 designed as an extrusion nozzle is inserted up to the shoulder.
  • Each of the stock dispensing nozzles 80 which are located in the first process chamber 12 and shown in FIGS. 8 and 9, have an axially inner narrower region which determines the diameter of a strand of doughy mass formed in the stock dispensing nozzle 80 and an axially outer enlarged region 84, which can be ventilated from the outside through at least one opening 86 in order to promote the drying of the strand.
  • an opening 86 is provided as an opening 86, which is arranged on the windward side of the material delivery nozzle 80 with respect to the general gas flow E and extends from the beginning of the enlarged area 84 to the free end of the material delivery nozzle 80.
  • the section of the lance 40 arranged in the first process chamber 12 also contains two lower compressed gas channels 94 parallel to the delivery channel 60, from which pressurized gas nozzles 96 extend in such a way that a pressurized gas nozzle 96 is directed onto the or an opening 86 of each material discharge nozzle 80.
  • the compressed gas channels 94 are intermittently supplied with compressed air, which can be dried and preheated, via electromagnetic valves of a known type.
  • the lower compressed gas nozzles 96 discharge compressed air intermittently onto the mouth area of the associated substance discharge nozzle 80.
  • the compressed air intermittently acts on the strand in a sharply bundled jet through the or a breakthrough in the associated material discharge nozzle 80, so that an extrudate particle H breaks off from it each time the compressed air blows.
  • a further compressed gas channel 98 is arranged, likewise parallel to the delivery channel 60, which is continuously supplied with warm, dry compressed air.
  • Compressed gas nozzles 100 emanate from the upper compressed gas channel 98 and are directed from above at an acute angle towards the respective mouth area of a material discharge nozzle 80.
  • the extrudate particle H formed therein is thus dried by a hot air jet and prevented by its pressure from breaking off prematurely before its free end has reached the end of the shield 88.
  • the broken-off extrudate particles H are carried upward in the first process chamber 12 by the general gas stream E, a fluidized bed F or fluidized bed forming in the trough 53 formed by the half-shells 52 and guide vanes 42 and 44, in which the extrudate particles H are further dried.
  • This fluidized bed F moves slowly but steadily forward on both sides of the lance 40 5 and 6 to the right, since the partial flows of the general gas flow E, which pass through the columns B, C and D, have a forward flow component.
  • This flow component arises from the fact that the guide vanes 42 and 44 and beads or ribs 102 projecting upwards into the half-shells 52, which rise to the left on both sides of the lance 40 and thus form a herringbone pattern with the direction of the arrow to the right in the plan view according to FIG. 5.
  • the guide vanes 42 and 44 and the half-shells 52 have the same shape and the same herringbone pattern as in the first process chamber 12.
  • the section of the lance 40 which extends through the middle process chamber 12 extends only for spraying the extrudate particles H and is equipped for this purpose with material discharge nozzles 80 in the form of multi-substance nozzles. These dispensing nozzles 80 are each arranged in a depression 104 at the upper edge of the lance profile and directed vertically upwards in the central plane A.
  • the associated middle section of the lance 40 is connected to a liquid line 106, a moist air line 108 and a dry air line 110.
  • the material delivery nozzles 80 fed by these lines generate a paint mist, e.g. from an aqueous or organic solution, suspension or dispersion, so that the extrudate particles H which are constantly moving forward in the fluidized bed F are coated.
  • a paint mist e.g. from an aqueous or organic solution, suspension or dispersion
  • Suitable multi-component nozzles are known from DE 3806537 A1, especially FIGS. 5 to 7.
  • the lacquered extrudate particles H are only dried while they continue to move forward.
  • the fluidized bed F that of the general one, can suffice for drying Gas flow E is generated in the trough 53.
  • the lance 40 can also be equipped with nozzles in the third process chamber 12, through which, for example, additional warm air is introduced into the fluidized bed F in order to promote drying.
  • the lacquered and dried extrudate particles H fall into a discharge chute 112.
  • the process chambers 12 are easily accessible for cleaning when the lids 28 are folded up.
  • the apparatus shown in Fig. 1 to 4 works in batches.
  • the lances 40 in all process chambers 12 are equipped with material discharge nozzles 80 in the form of multi-substance nozzles of the type known from DE 3806537 A1. According to FIG. 3, they are connected at their two ends to a liquid line 106, a moist air line 108 and a dry air line 110.
  • the guide vanes 42 and 44 and / or the half-shells 52 in turn have inclined beads or ribs 102 which, however, viewed from above, have the same inclination on both sides of the lance 40.
  • Such ribs 102 give the general gas flow E an oblique direction, so that the fluidized bed F on both sides of the lance 40 travels in opposite directions along the lance and the extrudate particles H are consequently mixed particularly well.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Drying Of Solid Materials (AREA)
  • Glanulating (AREA)
  • Steroid Compounds (AREA)
  • Detergent Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Housing For Livestock And Birds (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Paper (AREA)
  • Cereal-Derived Products (AREA)
  • Beans For Foods Or Fodder (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Pretreatment Of Seeds And Plants (AREA)
  • Furnace Charging Or Discharging (AREA)
  • Lubricants (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)
  • General Preparation And Processing Of Foods (AREA)
EP90120199A 1990-01-10 1990-10-22 Fliessbettapparatur zum Herstellen und/oder Weiterbehandeln schüttfähigen Gutes Expired - Lifetime EP0436787B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4000572A DE4000572C1 (fi) 1990-01-10 1990-01-10
DE4000572 1990-01-10

Publications (3)

Publication Number Publication Date
EP0436787A2 EP0436787A2 (de) 1991-07-17
EP0436787A3 EP0436787A3 (en) 1991-12-18
EP0436787B1 true EP0436787B1 (de) 1992-12-30

Family

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EP90120199A Expired - Lifetime EP0436787B1 (de) 1990-01-10 1990-10-22 Fliessbettapparatur zum Herstellen und/oder Weiterbehandeln schüttfähigen Gutes

Country Status (20)

Country Link
US (1) US5145650A (fi)
EP (1) EP0436787B1 (fi)
JP (1) JPH04215831A (fi)
KR (1) KR910014144A (fi)
AT (1) ATE83947T1 (fi)
AU (1) AU620739B2 (fi)
BR (1) BR9005970A (fi)
CA (1) CA2028056A1 (fi)
DE (2) DE4000572C1 (fi)
DK (1) DK0436787T3 (fi)
ES (1) ES2036390T3 (fi)
FI (1) FI905705A (fi)
GR (1) GR3007062T3 (fi)
HU (1) HU207240B (fi)
IE (1) IE903819A1 (fi)
IL (1) IL96097A0 (fi)
NO (1) NO904567L (fi)
PT (1) PT95987A (fi)
YU (1) YU222090A (fi)
ZA (1) ZA908586B (fi)

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WO2003080827A2 (en) 2002-03-27 2003-10-02 Novozymes A/S Granules with filamentous coatings
DE102007025317A1 (de) 2007-05-31 2008-12-04 Süd-Chemie AG Vorrichtung zur Herstellung eines als Schalenkatalysator ausgebildeten geträgerten Edelmetallkatalysators
DE102007025442A1 (de) 2007-05-31 2008-12-11 Süd-Chemie AG Verfahren zur Herstellung eines Schalenkatalysators und Schalenkatalysator
DE102007025357A1 (de) 2007-05-31 2009-01-08 Süd-Chemie AG Verfahren zum Auftragen einer Washcoatsuspension auf eine Trägerstruktur
DE102007025356A1 (de) 2007-05-31 2009-01-08 Süd-Chemie AG Verfahren zur Herstellung eines Schalenkatalysators und Schalenkatalysator
DE102008059342A1 (de) 2008-11-30 2010-06-10 Süd-Chemie AG Schalenkatalysator, Verfahren zu seiner Herstellung sowie Verwendung
DE102008058971A1 (de) 2008-11-25 2010-07-15 Süd-Chemie AG Schalenkatalysator, Verfahren zu seiner Herstellung sowie Verwendung
DE102009012415A1 (de) 2009-03-10 2010-09-16 Süd-Chemie AG Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung
DE102009014541A1 (de) 2009-03-24 2010-09-30 Süd-Chemie AG Katalysatoranordnung zur Oxidation von Methanol zu Formaldehyd
DE102009018109A1 (de) 2009-04-20 2010-11-18 Süd-Chemie AG Verfahren zur Herstellung eines geträgerten Ag/Pd-Katalysators
DE102010026462A1 (de) 2010-07-08 2012-01-12 Süd-Chemie AG Verfahren zur Herstellung eines Schalenkatalysators und Schalenkatalysator

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US5656243A (en) * 1995-04-04 1997-08-12 Snamprogetti S.P.A. Fluidized bed reactor and process for performing reactions therein
US6312521B1 (en) 1998-12-14 2001-11-06 Primera Foods Corporation Apparatus and process for coating particles
US6209479B1 (en) 1998-12-30 2001-04-03 Aeromatic-Fielder Ag Apparatus for coating tablets
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DE19904147C2 (de) * 1999-02-03 2001-05-10 Herbert Huettlin Vorrichtung zum Behandeln von partikelförmigem Gut
CN1110294C (zh) * 1999-03-20 2003-06-04 王小伦 具有特殊滚筒结构的包衣机
DE10309989A1 (de) 2003-02-28 2004-09-16 Hüttlin, Herbert, Dr.h.c. Tunnelförmige Vorrichtung zum Behandeln von partikelförmigem Gut
EP1491252A1 (en) * 2003-06-26 2004-12-29 Urea Casale S.A. Fluid bed granulation process and apparatus
DE10345342A1 (de) * 2003-09-19 2005-04-28 Engelhard Arzneimittel Gmbh Verfahren zur Herstellung eines lagerstabilen Extraktes aus Efeublättern, sowie ein nach diesem Verfahren hergestellter Extrakt
EP1743530B1 (en) * 2005-07-15 2011-08-31 Unilever N.V. Iron fortified food product and additive
DE102007025444A1 (de) * 2007-05-31 2008-12-11 Süd-Chemie AG VAM-Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung
DE102007025223A1 (de) 2007-05-31 2008-12-04 Süd-Chemie AG Zirkoniumoxid-dotierter VAM-Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung
DE102007025443A1 (de) 2007-05-31 2008-12-04 Süd-Chemie AG Pd/Au-Schalenkatalysator enthaltend HfO2, Verfahren zu dessen Herstellung sowie dessen Verwendung
DE102007025315A1 (de) * 2007-05-31 2008-12-11 Süd-Chemie AG Katalysator zur selektiven Hydrierung acetylenischer Kohlenwasserstoffe und Verfahren zu seiner Herstellung
DE102007025362A1 (de) 2007-05-31 2008-12-11 Süd-Chemie AG Dotierter Pd/Au-Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung
DE102007039759B3 (de) * 2007-08-22 2009-04-09 Richard Denk Verfahren und Vorrichtung zum kontaminationsfreien Beschicken und Entleeren
DE102008046772A1 (de) * 2008-09-11 2010-03-18 Glatt Ingenieurtechnik Gmbh Verfahren und Vorrichtung zur Behandlung von feinkörnigem Material in einer Strahlschicht
DE202008017277U1 (de) 2008-11-30 2009-04-30 Süd-Chemie AG Katalysatorträger
PT2864031T (pt) * 2012-06-20 2017-03-20 Romaco Innojet Gmbh Dispositivo de escala variável para tratar um produto em forma de partículas
DE102018208930A1 (de) * 2018-06-06 2019-12-12 Glatt Gesellschaft Mit Beschränkter Haftung Vorrichtung und Verfahren zur Herstellung und Behandlung von Granulat sowie Adapterstutzen zur Verbindung eines ein Granulat erzeugenden Granulators und eines Fluidisierungsapparates
CN109608013B (zh) * 2018-11-14 2021-11-30 杭州职业技术学院 一种牛粪沼渣烘干设备

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Cited By (16)

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US8722565B2 (en) 2007-05-31 2014-05-13 Sued-Chemie Ip Gmbh & Co. Kg Method for applying a wash coat suspension to a carrier structure
DE102007025317A1 (de) 2007-05-31 2008-12-04 Süd-Chemie AG Vorrichtung zur Herstellung eines als Schalenkatalysator ausgebildeten geträgerten Edelmetallkatalysators
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DE102008058971A1 (de) 2008-11-25 2010-07-15 Süd-Chemie AG Schalenkatalysator, Verfahren zu seiner Herstellung sowie Verwendung
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DE102009012415A1 (de) 2009-03-10 2010-09-16 Süd-Chemie AG Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung
DE102009014541A1 (de) 2009-03-24 2010-09-30 Süd-Chemie AG Katalysatoranordnung zur Oxidation von Methanol zu Formaldehyd
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WO2012004334A2 (de) 2010-07-08 2012-01-12 Süd-Chemie AG Verfahren zur herstellung eines schalenkatalysators und schalenkatalysator
DE102010026462A1 (de) 2010-07-08 2012-01-12 Süd-Chemie AG Verfahren zur Herstellung eines Schalenkatalysators und Schalenkatalysator

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ATE83947T1 (de) 1993-01-15
NO904567D0 (no) 1990-10-23
ZA908586B (en) 1991-09-25
AU6569490A (en) 1991-07-11
DE4000572C1 (fi) 1991-02-21
DE59000697D1 (de) 1993-02-11
BR9005970A (pt) 1991-09-24
DK0436787T3 (da) 1993-03-29
YU222090A (sh) 1993-10-20
HU906553D0 (en) 1991-04-29
FI905705A (fi) 1991-07-11
PT95987A (pt) 1992-08-31
EP0436787A3 (en) 1991-12-18
NO904567L (no) 1991-07-11
US5145650A (en) 1992-09-08
GR3007062T3 (fi) 1993-07-30
ES2036390T3 (es) 1993-05-16
EP0436787A2 (de) 1991-07-17
FI905705A0 (fi) 1990-11-19
AU620739B2 (en) 1992-02-20
IE903819A1 (en) 1991-07-17
JPH04215831A (ja) 1992-08-06
HU207240B (en) 1993-03-29
HUT59332A (en) 1992-05-28
IL96097A0 (en) 1991-07-18
KR910014144A (ko) 1991-08-31
CA2028056A1 (en) 1991-07-11

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